[0001] The present invention refers to an apparatus for drying bottles, particularly of
the type used in combination with a machine for washing bottles in a bottling plant.
[0002] The large bottling plants generally comprise a series of automated apparatuses performing
the several operations of the bottling cycle, such as washing and drying the inside
of the bottles, filling, corking or capping, washing and drying the bottle outside,
labelling and packaging.
[0003] According to the prior art, the drying of the bottle external surfaces after the
washing step is generally performed by advancing the standing bottles by means of
a conveyor belt through streams of forced air directed around the bottle external
surfaces.
[0004] The drying apparatuses must ensure a complete drying of the whole external surface
of the bottle, without leaving areas that are not completely dried at the end of the
drying step, which areas could impair the success of the subsequent labelling step.
Moreover, in large bottling plants, said apparatuses must ensure a high drying speed,
to prevent undue delays in the bottling plant.
[0005] EP-A 1 028 300, upon which the preamble of claim 1 is based, discloses an apparatus
for drying bottles in which the bottles are simultaneously submitted to a rotary and
a translatory motion while passing through air streams coming from nozzles located
along the path. Other apparatuses operating according to the same principle are disclosed
for instance in FR-A 2 444 908, FR-A 2 573 187, FR-A 2 660 583 and US-A 2 501 367.
[0006] The apparatus disclosed in EP-A 1 028 300 provides for conveying the bottles on a
pair of conveyor belts, adjacent and parallel to each other and advancing at different
speeds in the same direction, the belts supporting the bases of such bottles so that
half base rests on one belt and half on the adjacent belt. Forced air is sent against
the moving bottles through delivery ducts arranged parallel to the belts conveying
the bottles and equipped with holes formed in the wall delimiting the ducts.
[0007] Such an arrangement ensures the complete drying of the bottles only with a relatively
long path and hence with relatively long drying times. This is due in part to the
pressure drop of the drying air when leaving the delivery ducts, such drop making
the air streams impinging on the bottles have a considerably lower pressure than the
air flowing in said ducts.
[0008] It is an object of the invention to improve the drying efficiency of an apparatus
of the above kind, so that the complete drying can be achieved with reduced length
paths, whereby shorter drying times and simpler structures are obtained.
[0009] To attain such object without employing complex structures, it is possible to increase
the flow rate of the drying air impinging onto the bottles or to increase the pressure
of the drying air streams.
[0010] Yet, too strong air streams, or streams at too high pressure, can interfere with
the advancing and simultaneous rotation of the bottles along the conveyor line, with
the risk of causing collisions among adjacent bottles or collisions of the bottles
against parts of the drying apparatus, with consequent delays along the bottling line.
[0011] Therefore, it is another object of the invention to obviate the above drawbacks,
by manufacturing an apparatus that, while achieving a high drying efficiency, ensures
the proper advancing of the bottles along the conveyor line, without risks of collisions
of the bottles with each other or with parts of the apparatus.
[0012] The above and other objects are achieved by the apparatus for drying bottles as claimed
in the appended claims.
[0013] According to the invention, in order to optimise the bottle drying, the channels
provided inside the drying air delivery ducts and feeding the discharge holes with
air have a flared, funnel shaped initial portion, allowing conveying the pressurised
air present in said ducts towards the corresponding discharge hole, thus limiting
the air pressure drop and consequently allowing sending highpressure and high-speed
air streams against the bottles.
[0014] In an embodiment of the invention, the holes discharging the drying air streams towards
the bottles are arranged in two parallel rows along the respective ducts and are preferably
arranged in staggered relationship. Thus a stronger and better distributed air stream
is sent onto the bottles, allowing complete drying during a path of reduced length.
[0015] In a preferred embodiment, in order to ensure the bottle stability while the bottles
advance along the conveyor line, said conveyor line is made of a pair of conveyor
belts with different surface characteristics. More particularly, it is advantageous
that the belt moving in the bottle advancing direction has a rougher surface and the
belt moving in the opposite direction has a smoother surface.
[0016] Always in order to ensure a proper advancing of the bottles through the drying air
streams, the air delivery ducts may be constructed so that said air streams are inclined
forward with respect to the bottle advancing direction. Thus, the pressurised air
impinges onto said bottles on their rear sides, with reference to the advancing direction,
and pushes the bottles during their motion along said conveyor line, keeping their
distances unchanged.
[0017] Some embodiments of the present invention will be better understood from the description
given by way of non-limiting example, with reference to the attached drawings, in
which:
- Figure 1 is a side view of the apparatus according to the invention, located past
a station for washing the bottles;
- Figure 2 is a sectional view along line II-II of the apparatus shown in Figure 1;
- Figure 3 is a schematic representation of the effect caused by the drying means of
the apparatus shown in Figure 1 onto a bottle surface;
- Figures 4 to 7 show a number of different shapes of the air discharge channels in
the apparatus shown in Figure 1;
- Figure 8 is a sectional view along line IV-IV of Figure 2;
- Figure 9 is a schematic sectional view of the channel arrangement in a second embodiment
of the invention.
[0018] With reference to Figure 1, apparatus 1 for drying bottles according to the invention
is disposed downstream a bottle washing station 50 and is integrated therewith.
[0019] Apparatus 1 and station 50 are mounted on a substantially parallelepiped base 3,
constituted by a box-shaped frame 3d and provided with a roof 3a, detachable side
walls 3b and a plurality of adjustable supporting feet 3c.
[0020] Washing station 50 and the means for bottle transfer from said washing station 50
to conveyor line 10 of apparatus 1 are substantially known and are similar to those
disclosed in EP-A 1 028 300, and therefore they will not be described.
[0021] Apparatus 1 comprises a conveyor line 10 guiding the bottles along drying means capable
of sending forced air streams towards the bottles.
[0022] The drying means comprise a pair of ducts 41 for delivering drying air, which ducts
are located alongside conveyor line 10. A pair of blowers 44 are further located on
roof 3 a for producing a flow of forced air inside ducts 41. Each blower 44 is equipped,
for each duct 41, with a hose 45 connected to a hub 46 secured to the duct. One hub
46 is mounted for instance near the upstream end of duct 41 and the other one is mounted
in a central portion of the duct.
[0023] Blowers suitable to this aim are for instance blowers or compressors ELMO manufactured
by Siemens AG.
[0024] Ducts 41 hang from roof 3a of base 3 through brackets 42, such that ducts 41 are
tilted downwards, in a vertical plane, in the bottle advancing direction. Advantageously,
brackets 42 have adjustable lengths, so that the positions of ducts 41 can be adjusted
in a vertical plane to suit bottles with different sizes.
[0025] The air streams are obtained through a plurality of discharge holes provided along
each duct 41 and oriented towards the bottle transit zone, so as to generate a laminar
air stream that licks the external surfaces of bottles 2 with a desired inclination.
[0026] A guide 29, adjustable both in height and horizontally through corresponding handle
grips 30, is located parallel to conveyor line 10 so as to keep the bottles in upright
position during the translation along the conveyor line, in co-operation with the
air streams coming from duct 41 on the opposite side of conveyor line 10.
[0027] To avoid interference with duct 41 located on the same side, guide 29 can stop in
correspondence of the end portion of that duct, if the latter ends at a level below
guide 29. In such position, bottles 2 will be kept in upright position by the air
streams only.
[0028] Referring now to Figure 2, conveyor line 10 along which bottles 2 advance between
said ducts 41 comprises a pair of conveyor belts 12, 13, adjacent and parallel to
each other, supporting the bases of bottles 2 with half a base resting on one belt
and the other half base resting on an adjacent belt. Conveyor belts 12, 13 move at
different speeds, preferably in opposite directions: in that case, the speed of belt
12 moving in the transfer direction of bottles 2 will be higher than that of belt
13 moving in the opposite direction. This way, during the advancing movement of the
belts, a rotary motion around their axes is also imparted to bottles 2.
[0029] Conveyor belts 12 and 13 are preferably made of a mesh of a resistant and inextensible
plastic material, and they run over supports 11, preferably made of box-type stainless
steel. Spacers 17 and 18 of a material having a low coefficient of friction are secured
to said supports and are arranged so that belts 12 and 13 are inclined by an angle
α, preferably in the range of about 1° to 5°, towards the centre line of the conveyor
line. Thus, the cross section of the conveying surface on which bottles 2 rest is
substantially V-shaped.
[0030] Always with reference to Fig. 2, it is clearly apparent that the positions and the
inclinations of ducts 41 along the conveyor line are such that the air streams arrive
at the region of cork or cap 2a in the initial portion of ducts 41 (position 1), at
the intermediate region between neck 2b and body 2c of bottles 2 in the central portion
of ducts 41 (position 2), and at the region adjacent to bases 2d of bottles 2 in the
end portion of ducts 41 (position 3).
[0031] Thanks to the rotary motion of bottles 2 and to the inclination of ducts 41, while
bottles 2 advance along conveyor line 10, a spiral drying effect, from top to down,
is obtained, which drags downward the film of water covering bottles 2 and ensures
a complete drying of the whole external surfaces of bottles 2.
[0032] The air streams are discharged from ducts 41 through a plurality of discharge holes
43.
[0033] Said holes 43 do not open directly into the body of the respective duct 41, but they
are formed at the ends of respective channels 47 provided in a spout 48, extending
along the whole lower comer of duct 41 and projecting towards bottles 2. Said spout
48, when seen in cross section, has a greater length in the initial zone of duct 41
(position 1). Thus holes 43 are at the proper distance from the concerned region of
bottle 2 at any position along the bottle travel, and spacing apart ducts 41 in the
area where the bottles leave the apparatus (position 3) is not required.
[0034] Referring to Figure 3, there is schematically shown the effect caused by the air
coming from holes 43 onto the surface of the bottle advancing in direction F, in a
preferred arrangement of said holes.
[0035] Reference symbols A1 - A5 denote the areas licked by the air discharged from the
holes on a plane spaced by about 1.5 cm from the bottle surfaces. It can be appreciated
that discharge holes 43 are mutually spaced so that there is an overlap between adjacent
areas on which air impinges while the bottles advance.
[0036] Overlapping areas Z1...Z4 form a security margin in order to obtain an optimum drying
effect. Indeed, the bottle portions corresponding to such overlapping areas will be
dried not only by the air stream coming from the first hole, but also by the subsequent
one.
[0037] As better shown in Fig. 4, according to the invention channels 47 feeding said discharge
holes 43 with air have a non-uniform cross section.
[0038] More particularly, in the embodiment shown, the channels comprise, in the air advancing
direction, a first cylindrical portion 471, a flared portion 472 and a second cylindrical
portion 473 of smaller diameter than the first cylindrical portion 471.
[0039] The particular shape of channels 47, and in particular the provision of a flared
portion, allows reducing the pressure drop of the drying air when passing in said
channels. Consequently, for a given pressure of air in ducts 41, it is possible to
send, against the bottles to be dried, air streams at higher pressures and higher
speeds than attainable with cylindrical channels of uniform cross section.
[0040] This way, drying efficiency is improved and it is possible to reduce the length of
the bottle drying path and the bottle drying time.
[0041] In an exemplary embodiment, the ratio of the diameter of said first cylindrical portion
471 to the diameter of said second cylindrical portion 473 is preferably less than
5. Moreover, the second cylindrical portion 473 of channel 47 has a substantially
greater length than the sum of the lengths of the first cylindrical portion 471 and
the flared portion. Preferably, the ratio of said lengths is about 2.75. Moreover,
said first cylindrical portion has about the same length as the flared portion.
[0042] For instance, said channels 47 may have an overall length of the order of 1.5 cm,
with a first cylindrical portion 471 0.2 cm long, a flared portion also 0.2 cm long
and a second cylindrical portion 1.1 cm long. The first cylindrical portion 471 may
have a diameter of about 1 cm, whereas the second cylindrical portion 473 may have
a diameter in the range 0.2 to 0.8 cm.
[0043] Other possible shapes of the air discharge channels that can be constructed without
departing from the scope of the invention are shown in Figures 5 to 7.
[0044] In the variant shown in Fig. 5, air discharge channels 57 comprise, in the air advancing
direction, a flared portion 572 that directly opens into duct 41 and is followed by
a cylindrical portion 573 of which the diameter is smaller than the maximum diameter
of said flared portion and preferably is substantially the same as the minimum diameter.
The cylindrical portion ends in air discharge hole 53.
[0045] Preferably, the ratio of the maximum diameter of said flared portion 572 to that
of said cylindrical portion 573 is less than 5, and the ratio of the length of said
cylindrical portion 573 to that of said flared portion 572 is about 1.55.
[0046] For instance, said channels 57 may have an overall length of the order of 1.5 cm,
with a flared portion 0.59 cm long and a cylindrical portion 0.91 cm long. The flared
portion may have a maximum diameter of about 1 cm and a minimum diameter of about
0.3 cm.
[0047] Air discharge channels 67 made in accordance with the variant shown in Fig. 6 comprise,
in the air advancing direction, a flared portion 672, an intermediate frusto-conical
portion 674 and a cylindrical portion 673 ending in air discharge hole 63. Intermediate
frusto-conical portion 674 has a maximum diameter equal to the minimum diameter of
flared portion 672, and cylindrical portion 673 has a diameter that is substantially
the same as the minimum diameter of said flared portion.
[0048] Preferably, the ratio of the maximum diameter of said flared portion 672 to the diameter
of said cylindrical portion 673 is less than 5, and the ratio of the sum of the lengths
of said cylindrical portion 673 and said frusto-conical portion 674 to the length
of said flared portion 672 is about 2.
[0049] For instance, said channels 67 may have an overall length of the order of 1.5 cm,
with a flared portion 0.5 cm long, a frusto-conical portion about 0.6 cm long and
a cylindrical portion about 0.4 cm long. Flared portion 672 may have a maximum diameter
of about 1 cm and a minimum diameter of about 0.42 cm, whereas the second cylindrical
portion 473 may have a diameter of about 0.3 cm.
[0050] Lastly, according to the variant shown in Fig. 7, air discharge channels 77 comprise,
in the air advancing direction, a flared portion 772 and a frusto-conical portion
774 ending in air discharge hole 73.
[0051] Preferably, the maximum diameter of said frusto-conical portion 774 is the same as
the minimum diameter of flared portion 772. Moreover, the ratio of the maximum diameter
of said flared portion 772 to the minimum diameter of said frusto-conical portion
774 is less than 5, and the ratio of the length of said frusto-conical portion 774
to the length of said flared portion 772 is about 2.
[0052] For instance, said channels 77 may have an overall length of the order of 1.5 cm,
with a flared portion 0.5 cm long and a frusto-conical portion 774 about 1 cm long.
Flared portion 772 may have a maximum diameter of about 1 cm and a minimum diameter
of about 0.42 cm, whereas the frusto-conical portion 774 may have a minimum diameter
of about 0.25 cm.
[0053] As a general indication, a good performance in terms of drying efficiency is obtained
by using channels with a length in the range 0.5 to 3.5 cm, ending in an air discharge
hole with a diameter in the range 0.1 to 0.8 cm and comprising a flared portion with
a length in the range 0.25 to 1.5 cm and a maximum diameter in the range 0.25 to 1.5
cm.
[0054] Referring to Fig. 8, in order to improve the bottle drying efficiency, the air streams
are generated by at least two sets of channels 47 provided with respective discharge
holes 43 arranged in staggered relationship in at least two parallel rows along each
duct 41. It is thus possible considerably to increase the number of holes per length
unit of the path run by the bottles, thereby further reducing the drying time and
the drying path length.
[0055] Referring to the above mentioned example, the distance between said parallel rows
may be in the range 0.3 to 1.5 cm and the distance between two successive holes in
a same row may be in the range 0.5 to 2.5 cm.
[0056] It is clear that the features described above entail a considerable reduction in
the drying time and the drying path length. It is also clear that, in order to create
the spiral drying effect on the bottles over a greatly reduced length, ducts 41 should
have a much greater inclination relative to the plane of conveyor line 10 on which
the bottles advance.
[0057] Yet, the great inclination of ducts 41 and the high pressure of the air discharged
from holes 43 can lead to an irregular advancing of the bottles along conveyor line
10 and to the consequent risk of collisions. For a good operation of the apparatus
it is on the contrary necessary that the distance between the bottles does not change
during drying and that it is kept within security limits to avoid breakings.
[0058] To obviate such drawback, the surfaces of conveyor belts 12, 13 in contact with the
bottoms of bottles 2 are made different so that they have different friction coefficients
with respect to the bottle glass surfaces. More particularly, belt 12 moving in the
same direction as bottles 2 has a surface of which the adhesion with respect to the
glass of bottles 2 is greater than that of belt 12 moving in the opposite direction.
[0059] Such a difference may be obtained by using different materials for belts 12, 13,
or by submitting one of the belts to a chemical or mechanical process (e.g. grinding)
changing its roughness.
[0060] That solution ensures the proper advancing of bottles 2 between air delivery ducts
41 even in case of very short drying paths with greatly inclined ducts 41 and high
air discharge pressures.
[0061] It is to be appreciated that such a feature may be advantageously employed not only
in the apparatus of the invention, but also in all known apparatuses in which the
bottles to be dried are placed on a pair of conveyor belts advancing at different
speeds, in order to increase the stability of said bottles.
[0062] Fig. 9 shows a second embodiment of the invention that, in order to solve the problem
of avoiding the irregular advancing of the bottles, uses channels 47 inclined forward
with respect to the advancing direction of bottles 2.
[0063] Thus, the air streams coming from said holes 43 impinge on the surfaces of bottles
2 on the rear sides 2e with reference to the advancing direction of said bottles and,
besides providing for the complete drying of bottles 2, said streams assist in pushing
the bottles along conveyor line 10, thereby helping in reducing the risk of collisions
with adjacent bottles.
[0064] The skilled in the art will appreciate that such a feature may be advantageously
employed not only in the apparatus of the invention, but also in all known apparatuses
in which the bottles are dried by means of pressurised air streams.
[0065] Thus, it is clear that in all embodiments disclosed the apparatus of the invention
allows improving the bottle drying efficiency, by limiting the drying path length
and the drying time, without thereby negatively affecting the proper advancing of
the bottles along the drying path or entailing the risk of undue delays on the bottling
line.
[0066] It is also clear that the above description is given only by way of non limiting
example and that changes and modifications are possible without departing from the
scope of the invention.
1. An apparatus (1) for drying the external surfaces of bottles (2), comprising means
(10, 12, 13) for conveying the bottles (2) along drying means (41) and for imparting
to the bottles a rotary motion about their axes, the drying means comprising a pair
of ducts (41) for delivering forced air streams, which ducts are located along at
least one side of the bottle path, are downwards inclined in the advancing direction
of the bottles (2) and are equipped with a plurality of holes (43; 53; 63; 73) for
discharging air towards the bottles (2), each said hole (43) being fed with air through
a channel (47; 57; 67; 77) formed inside the respective duct (41) and oriented so
that the stream discharged from the respective hole (43; 53; 63; 73) is sent towards
the bottle, characterised in that said channel comprises a flared initial portion (472; 572; 672; 772) flaring in the
air discharge direction.
2. An apparatus (1) as claimed in claim 1, characterised in that said channels (47) comprise, in the air discharge direction, a first cylindrical
portion (471), a flared portion (472) and a second cylindrical portion (473), the
channel diameter decreasing in the air advancing direction.
3. An apparatus (1) as claimed in claim 2, characterised in that the length of said second cylindrical portion (473) is at least twice the sum of
the lengths of said first cylindrical portion (471) and said flared portion (472).
4. An apparatus (1) as claimed in claim 2 or 3, characterised in that the length of said first cylindrical portion (471) is the same as the length of said
flared portion (472).
5. An apparatus (1) as claimed in claim 1, characterised in that said channels (57) comprise, in the air discharge direction, a flared portion (572)
and a cylindrical portion (573), the channel diameter decreasing in the air advancing
direction.
6. An apparatus (1) as claimed in claim 5, characterised in that the length of said cylindrical portion (573) is at least equal to the length of said
flared portion (572).
7. An apparatus (1) as claimed in claim 1, characterised in that said channels (67) comprise, in the air discharge direction, a flared portion (672),
a frusto-conical portion (674) and a cylindrical portion (673), the channel diameter
decreasing in the air advancing direction.
8. An apparatus (1) as claimed in claim 7, characterised in that the sum of the lengths of said frusto-conical portion (674) and said cylindrical
portion (673) is about twice the length of said flared portion (672).
9. An apparatus (1) as claimed in claim 1, characterised in that said channels (77) comprise, in the air discharge direction, a flared portion (772)
and a frusto-conical portion (774), the channel diameter decreasing in the air advancing
direction.
10. An apparatus (1) as claimed in claim 9, characterised in that the length of said frusto-conical portion (774) is about twice the length of said
flared portion (772).
11. An apparatus (1) as claimed in claim 1, characterised in that the ratio of the maximum diameter of said flared portion (472; 572; 672; 772) to
the diameter of said air discharge hole (43; 53; 63; 73) is less than 5.
12. An apparatus (1) as claimed in claim 1, characterised in that said channels (47; 57; 67; 77) have a length in the range 0.5 to 3.5 cm and end in
an air discharge hole (43; 53; 63; 73) with a diameter in the range 0.1 to 0.8 cm,
said channels having a flared portion (472; 572; 672; 772) of which the length is
in the range 0.25 to 1.5 cm and the maximum diameter is in the range 0.25 to 1.5 cm.
13. An apparatus (1) as claimed in claim 1, characterised in that the distance between two successive holes (43; 53; 63; 73) on said duct (41) is chosen
so that the area impinged on by the air coming from a channel on the surfaces of the
advancing bottles partly overlaps with the area impinged on by the air coming from
the adjacent channel.
14. An apparatus (1) as claimed in claim 1, characterised in that said conveyor means comprise a pair of conveyor belts (12, 13) disposed adjacent
and parallel to each other, on which the bases of the bottles (2) rest so that half
a base is supported by one belt (12) and the other half base is supported by the adjacent
belt (13), a first one (12) of said two belts moving in the direction of conveyance
of the bottles (2) and the second belt (13) moving in opposite direction to and at
a lower speed than the first one (12).
15. An apparatus (1) as claimed in claim 14, characterised in that the surfaces of said first and second belts (12, 13) have different friction characteristics.
16. An apparatus (1) as claimed in claim 15, characterised in that the friction coefficient of said first belt (12, 13) with respect to the bottles
is higher than that of said second belt (12, 13).
17. An apparatus (1) as claimed in claim 1, characterised in that said friction difference is obtained by submitting said first belt (12) and/or said
second belt (13) to a chemical and/or mechanical process.
18. An apparatus (1) as claimed in claim 1, characterised in that said channels (47; 57; 67; 77) are inclined forward with respect to the advancing
direction of said bottles (2) on said conveyor means.
19. An apparatus (1) as claimed in any preceding claim, characterised in that said holes (43; 53; 63; 73) are arranged in staggered relationship on at least two
parallel rows along said ducts (41).
20. An apparatus (1) as claimed in any preceding claim, characterised in that said ducts (41) are so arranged that the holes (43; 53; 63; 73) in an initial portion
of the ducts (41) send their streams in correspondence of the corks (2a) of the bottles
(2), and the holes (43) in a final portion of the ducts (41) send their streams in
correspondence of the bottoms (2d) of the bottles (2).
21. An apparatus (1) as claimed in any preceding claim, characterised in that said ducts (41) are mounted so that they are adjustable in height.
22. An apparatus (1) as claimed in any preceding claim, characterised in that said ducts (41) have a main body and a spout (48) extending along the whole of the
main body and transversally projecting from said body towards the bottles (2) conveyed
on said conveyor means (10, 12, 13), and said channels (47; 57; 67; 77) are formed
in said spout (48).
23. An apparatus (1) as claimed in claim 22, characterised in that said spout (48) has a greater transversal size in said initial portion of the ducts
than in the remaining portion of the respective duct (41).